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A comparison between model predictions and observations from laboratory scale UCG experiments on the same coal shows an excellent match for both exit gas quality and cavity growth.
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Furnace exit gas temperature (FEGT) is one such important design/operating parameter.
The SO3 decomposition percentage was determined using the measured O2 concentration in the exit gas stream.
Char reactivity is evaluated from the time variation of CO concentration in the exit gas.
Moreover, the exit gas is an almost pure CO2 stream, requiring little or no gas separation before compression for sequestration.
In addition, discussions of peak and exit gas temperature trends are included.
The concentration of N2 in the fuel reactor exit gas increases with the fuel reactor temperature.
The transient temperature profile in the descending bed as well as the exit gas composition is presented here.
There are various techniques used to scrub the exit gas, such as packed columns, spray scrubbers, fluidised beds, filters, etc.
The exit gas from the fuel reactor is CO2 and H2O.
Thermal energy in the exit gas from the rotary kiln is recovered by application of a preheater.
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